# US 5,705,073 A · Method for the disposal of excess sludge

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- Number: US 5,705,073 A
- Document ID: US5705073A
- Status: Granted
- Kind: A
- Application number: 08/491,863
- Filed: 1995-08-09
- Granted: 1998-01-06
- Earliest claimed: 1992-12-24
- Assignees: Austrian Energy & Environment SGP/Waagner Biro GmbH
- Inventors: Heinz Loquenz; Wolfgang Glaser; Kurt Tamandl; Peter Yaldez
- Web page: https://patentgrep.com/patent/US5705073A

## CPC

- C02F 9/00: Multistage treatment of water, waste water or sewage
- C02F 3/1215: {Combinations of activated sludge treatment with precipitation, flocculation, coagulation and separation of phosphates}
- C02F 1/5236: {using inorganic agents}
- C02F 1/66: by neutralisation; pH adjustment (for degassing C02F1/20; using ion-exchange C02F1/42; for flocculation or precipitation of suspended impurities C02F1/52; for removing dissolved compounds C02F1/58)
- C02F 11/06: by oxidation (incinerators for burning waste liquors, e.g. sulfite liquor from paper-making plant F23G7/04)
- C02F 2103/28: from the paper or cellulose industry
- Y02W 10/10: Biological treatment of water, waste water, or sewage
- Y02W 10/40: Valorisation of by-products of wastewater, sewage or sludge processing
- Y10S 210/928: Paper mill waste, e.g. white water, black liquor treated
- C02F: TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE (separation in general B01D; special arrangements on waterborne vessels of installations for treating water, waste water or sewage, e.g. for producing fresh water, B63J; adding materials to water to prevent corrosion C23F; treating radioactively-contaminated liquids G21F9/04; regeneration of reactants for recirculation into processes, see the relevant places for the processes)
- Y02W: CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y10S: TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS

## Abstract

A method for incinerating excess sludge from biological waste water treatment plants, in particular sludges arising from the manufacture of paper or paper pulp, preferably using the magnesium fusion process. Before incineration, the excess sludge is neutralized with the same base as used in the paper pulp process and the dust entrained by the combustion gas is precipitated to recover the base.

## Claims

### Claim 1

Method for disposing of sludge produced during waste water treatment in biological waste-water treatment plants with waste water neutralization operating with a magnesium oxide disintegration process for paper or paper pulp production plants comprising the steps of:
neutralizing the waste water with a base before it enters an activated sludge installation in which sludge is produced,
utilizing the same base for digestion of the paper pulp,
incinerating the sludge directly or first mixing the sludge with a liquid fuel and then incinerating the mixture to generate a combustion exhaust gas,
separating dust entrained in the combustion exhaust gas, and
utilizing the dust or the neutralization product contained in the dust at least in part for the neutralization of the waste water.

### Claim 2 (depends on 1)

The method of claim 1, wherein the neutralized sludge is incinerated in a lye-burning furnace, further comprising the step of providing the dust from the combustion exhaust gas to absorb SO.sub.2 contained in the combustion exhaust gas.

### Claim 3 (depends on 1)

The method of claim 1, further comprising the step of concentrating the sludge mixture to be incinerated to about 50% to 70% ACTS before combustion.

### Claim 4 (depends on 1)

The method of claim 1, wherein the sludge is mixed with a waste lye and the mixture then incinerated, further comprising the step of setting the waste lye to a pH value greater than about 9 before the admixture of the sludge.

### Claim 5 (depends on 1)

The method of claim 1, further comprising the step of leaching or sieving the dust entrained by the combustion exhaust gas before being the dust is used for the reclamation of MgO and removal of undesirable accompanying materials.

### Claim 6 (depends on 1)

The method of claim 1, wherein the sludge is mixed with a waste lye and the mixture concentrated and then incinerated in a waste lye incineration furnace, and the dust from the combustion exhaust gas from said incineration furnace is used at least in part for the neutralization of the waste water and for disintegration of the pulp.

### Claim 7 (depends on 1)

The method of claim 1, wherein the sludge is incinerated directly.

### Claim 8 (depends on 1)

The method of claim 1, wherein the sludge is first mixed with a waste lye and then incinerated to generate the combustion exhaust gas, said exhaust gas comprising dust.

### Claim 9 (depends on 6)

The method of claim 6, said accompanying materials comprising a compound selected from the group consisting of CaSO.sub.3 and CaCO.sub.3.